Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/12—Powdering or granulating
  • C08J3/14—Powdering or granulating by precipitation from solutions
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2377/00—Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers

Definitions

• the modified polyamides which, in accordance with this invention may be prepared in granular form, are the N-alkoxy-methyl polyamides. These may be prepared by condensation of an aldehyde and'an alcohol with a synthetic polyamide as described in the copending applications of T. L. Cairns, S. N. 445,635, filed June 3, 1942, and S. N. 507.745, filed October 26, 1943, and also in the copending application of H. D. Foster. and A. W. Larchar, S. N. 503,130, filed September20, 1943.
• the improvements provided by the present invention are concerned particularly with methods for isolating the N-alkoxymethyl polyamides' in finely divided granular form.
• the average number of carbon atoms in the segments of the chain separating the amide groups is at least two.
• a dissolved N- 5 alkoxymethyl polyamide made by acid condensation of a polyamide with formaldehyde and an alcohol, is first neutralized with an alkaline reagent, and is thereafter treated with controlled amounts of water while stirring rapidly in producing a dispersion.
• This dispersion on prolonged stirring agglomerates, but as the stirring continues the agglomerated resin'redisperses in the form of fine solid particles. hardens the particles into firm granules which are readily separated from the mother liquor by conventional means, such as,-decantation, filtration, or centrifugation.
• The-condensation of'polyamides with formaldehyde and alcohols may be effected by treating a polyamide, such as polyhexamethylene adipamide, with an excess of formaldehyde and an alcohol in the presence of an oxygen containing acid catalyst, suitably with agitation in a closed vessel at 100 to 150 C.
• Phosphoric acid is the pre- 5 ierred acid-reacting catalyst.
• the amount of catalyst should be about 1 to 10% of the weight of polyamide used. Good results are obtained when one part of formaldehyde and one to two parts of alcohol are charged per part of polyamide. Since the reaction is rapid, proper control is best obtained by keeping the reaction mixture alkaline or neutral until the precise time at which it is desired to start the condensation.
• a reaction mixture which gives good results has the following composition, parts being by weight:
• the polyamide is minimized and by controlling the amount of-water and aldehyde present, the deree of substitution may be varied.
• the deree of substitution may be varied.
• the reaction is stopped by lowering the reaction temperature and decreasing the catalystconcentration, for example, by withdrawing the reaction mixture into a quenching redispersion occurs, and thereafter adding a furbath containing chiefly methanol, but which may Additional water also contain water and an alkaline material, preferably ammonia.
• a satisfactory quench contains:
• At least enough ammonia should preferably be present to neutralize the condensation catalyst. Any unreacted formaldehyde may also react with the excess ammonia, forming hexamethylenetetramine.
• the resulting product is in main a solution of N-alkoxymethyl polyamide in the alcohol. Any solid impurities that may be present may be removed from the cooled solution by filtration or centrifuging. The resulting clear solution must be used promptly in the next operation, else gelation will occur.
• the granulation operation is conducted as follows.- In the first stage, water (for example, about 68 pounds per 100 pounds of the solution) is slowly introduced in the form of fine streams into the agitated solution. The result is a white slime which disperses throughout the mixture. In the second stage no further water is added but the stirring continues, and as aresult the dispersion agglomerates. As the stirring continues, the agglomerated mass breaks up and redisperses. In the final stage an additional quantity of water and approximately132 pounds per 100 pounds of quench liquor is added, with continued stirring, whereby the dispersed particles harden into small white granules.
• the particle size may be controlled by varying the degree and time of agitation in the interval between-the start of granulation (redispersion) and the introduction of the second-stage water. With the proportions given above, precipitation'is about 98% complete.
• the polymer can be separated from the mother liquor by conventional means such as decantation, filtration, or centrifugation. Use of a centrifuge is preferred.
• the polymer was thoroughly washed and was then dried at C. to give a white granular freeflowing product. .It contained 7.9% by weight of methoxyl groups, 1.4% methylol groups. and was soluble in hot 80% ethanol. A film prepared by casting a solution of this polymer was tough and transparent.
• polyamides which may be treated by the general method described above include polyhexamethylene adipamide, polyhexamethylene sebacamide, and polyamides derived from epsilonamino-caproic acid.
• polyamides are linear synthetic resins having a recurring group (X being oxygen or sulfur). Interpoiymers of such polyamides may also be used.
• X being oxygen or sulfur
• suitable alcohols being methanol, ethanol, isopropanol, n-propanol and allyl alcohol. It is not necessary, although it is usually preferred, to use the same alcohol in the quenching bath as in the condensation mixture.
• the acidreacting condensation catalyst include formic,
• Control over the degree of substitution of the carbonamide hydrogens may be by any convenient method, such as by limiting the ratio of alcohol or formaldehyde to polyamide in the reaction mixture. Increasing the water content of the condensation mixture usually is effective in reducing the amount of substitution.
• substitution and decomposition reactions is the precise control of the time that the reaction mixture remains acidic and at reaction temperature. This can be done most effectively by keeping the reaction mixture alkaline up to the time at which the reaction is to take place, at which time the catalyst is rapidly added. The reaction is quickly stopped by dilution, cooling, and/or neutralization of the acid catalyst.
• the condensation reaction may be conducted in any suitable apparatus, such as a stirred autoclave, made of or lined with acid-resisting materials including nickel, stainless steel, silver, glass,
• the granulation method herein disclosed is most effective with N-alkoxymethyl polyamides which are readily soluble in alcohol, and preferably in which the polyamides have between 20 and 45% of the carbonamide hydrogens substituted by the alkoxymethyl groups.
• the method is less effective when the de ree of carbonamide substitution is high (45 to 50%), because these resins, after precipitation, redisperse with considerable difficulty.
• the N-alkoxymethyl polyamide solutions from which the modified polyamides are precipitated by the method of this invention contain less than 25% polymer.
• the amount of water added during the first stage of the granulation operation must be carefully controlled so as to yield not a hardened resin but a dispersion of soft slime. The amount of water required for this varies with the alcohol content of the solution, and also with the N-alkoxymethyl content of the resin. The higher the N-alkoxymethyl content of the resin, the larger is the amount of water required to produce the desired dispersion.
• the granular N-alkoxymethyl polyamides prepared in accordance with this invention are useful in the manufacture of molded products, foils,
• the N-alkoxymethyl polyamides may be used in compositions containing other resin ingredients such as urea, melamine, methylene diurea, thiourea, etc., or the methylol or alkoxymethyl derivatives of these compounds.
• a process for preparing granular N-alkoxymethyl polyamides which comprises condensing a polyamide at a temperature of 100 to 155 C. with formaldehyde and a monohydric alkanol having not more than three carbon atoms in the presence of an acid condensation catalyst of the class consisting of phosphoric, formic, acetic, oxalic, trimethylacetic, benzoic, sulfuric, p-toluene-sulfonic, hydroxyacetic and maleic acids, said polyamide being a linear polymer in which all of the amide groups are combined in the form of intralinear carbonamide groups of the formula recurring along the chain, the average number of carbon atoms in the segments separating the amide groups of the chain being at least 2, continuing the condensation reaction until 20% to 45% of the carbonamide hydrogens have been substituted by alkoxymethyl groups, quenching the resulting solution of the condensation product by mixing it with an alcoholic solution containing a sufiicient quantity of ammonia to neutralize the
• a process for preparing granular N-alkoxy-' methyl polyamides which comprises condensing a polyamide with formaldehyde and a monohydric alkanol having not more than three carbon atoms in the presence of an acid condensation catalyst of the class'consisting of phosphoric, formic, acetic, oxalic, trimethylacetic, benzoic, 'surfuric.
• said polyamide being a linear polymer in which all of the amide groups are combined in the form of aqueous ammonia, said solution containing sufflcient ammonia to neutralize the condensation catalyst, adding slowly with agitation a controlled amount of water to the thus quenched solution containing less than 25% of the alkoxymethyl polyamide whereby a slimy dispersion is produced, stopping the addition of water, and agitating the slimy dispersion until it agglomerates, thereafter continuing the agitation whereby the resulting agglomerated mass redisperses, adding a further quantity of water which hardens the redispersed particles, and separating the hardened particles from the mother liquor.
• a process for preparing granular N-methoxymethyl polyhexamethylene adipamides which comprises condensing polyhexamethylene-adipamide with formaldehyde and methanol at a temperature of100 to 150 C. in the presence of an acid condensation catalyst of the class consisting of phosphoric, formic, acetic, oxalic, trimethylacetic, benzoic, sulfuric, p-toluenesulfonic, hydroxyacetic and maleic acids until 20 to 45% of the carbonamide hydrogens have been substituted by methoxymethyl groups, quenching the a resulting solution of condensation product by glomerated mass redisperses, adding a further mixing it with a methanolic solution of aqueous ammonia, said solution containing enough am-l monia to neutralize the condensation catalyst,

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• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Phenolic Resins Or Amino Resins (AREA)

Priority Applications (5)

Applications Claiming Priority (1)

Publications (1)

Family

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Family Applications (1)

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Cited By (8)

Citations (3)

• 0
  • BE BE468087D patent/BE468087A/xx unknown
• 1944
  • 1944-02-09 US US521658A patent/US2430866A/en not_active Expired - Lifetime
• 1946
  • 1946-09-09 FR FR937958D patent/FR937958A/fr not_active Expired

Patent Citations (3)

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